Dual-Acid-Site Engineering in Ti-β Zeolites for Enhanced Benzene Alkylation with Cyclohexene

化学 烷基化 环己烯 催化作用 有机化学 烯烃纤维 沸石 路易斯酸 硅醇 质子化 无机化学 高分子化学 吸附 热稳定性 光化学 溶剂 环己烷 酸催化 碳氢化合物 烯烃 多相催化 组合化学
作者
Wenfeng Lang,Hao Li,Longzhou Zhang,Jie Feng,Yongheng Jia,Mengting Zhang,Shufang Zhao,Young Dok Kim,Zheng Liu,Zhikun Peng
出处
期刊:ACS Sustainable Chemistry & Engineering [American Chemical Society]
卷期号:14 (1): 229-237
标识
DOI:10.1021/acssuschemeng.5c09374
摘要

The alkylation of benzene with cyclohexene provides a direct and atom-efficient route to cyclohexylbenzene (CHB), a key intermediate for advanced chemical manufacturing. The role of Lewis acid sites (LAS) in homogeneous alkylation is well established; however, their function and synergy with Brønsted acid sites (BAS) in solid acid catalysts remain elusive. Herein, we proposed a dual-acid-site engineering strategy to construct titanium-incorporated β zeolites (Hβ-at-x) via sequential dealumination and titanation. Structural and spectroscopic characterizations confirmed that Ti was anchored in silanol nests, generating electron-deficient Ti-LAS while tuning the Al-BAS to establish synergetic dual-acid-site. It was demonstrated that Ti-modified Al-BAS facilitated the protonation of cyclohexene, and benzene was adsorbed and enriched on Ti-LAS via π-complexation adjacent to BAS. The optimized Hβ-at-50 catalyst achieved complete cyclohexene conversion, even under the currently lowest benzene-to-cyclohexene volume ratio of 7:1. Furthermore, it demonstrated a significantly enhanced CHB formation rate of 18.6 mmolCHB·gcat–1·h–1, surpassing that of the parent Hβ catalyst (2.98 mmolCHB·gcat–1·h–1) and the Hβ-at catalyst (2.29 mmolCHB·gcat–1·h–1). The superior activity was corroborated by a reduced apparent activation energy (Ea = 35.1 kJ·mol–1) compared to the parent Hβ catalyst (Ea = 57.3 kJ·mol–1). The catalytic stability decreased during cycling due to the light olefin polymerization, and its activity could be fully restored via thermal treatment. This work provides mechanistic insight into dual-site catalysis and a design framework for high-performance zeolite catalysts for hydrocarbon upgrading.
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